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Variation of activity

Considering first pure nitric acid as the solvent, if the concentrations of nitronium ion in the absence and presence of a stoichiometric concentration x of dinitrogen tetroxide are yo and y respectively, these will also represent the concentrations of water in the two solutions, and the concentrations of nitrate ion will be y and x- y respectively. The equilibrium law, assuming that the variation of activity coefficients is negligible, then requires that ... [Pg.221]

Fig. 8. Variation of activation energy with kinetic molecular diameter for diffusion in 4A 2eohte (A), 5A 2eohte (0)> carbon molecular sieve (MSC-5A) (A). Kinetic diameters are estimated from the van der Waals co-volumes. From ref. 7. To convert kj to kcal divide by 4.184. Fig. 8. Variation of activation energy with kinetic molecular diameter for diffusion in 4A 2eohte (A), 5A 2eohte (0)> carbon molecular sieve (MSC-5A) (A). Kinetic diameters are estimated from the van der Waals co-volumes. From ref. 7. To convert kj to kcal divide by 4.184.
Standard potentials Ee are evaluated with full regard to activity effects and with all ions present in simple form they are really limiting or ideal values and are rarely observed in a potentiometric measurement. In practice, the solutions may be quite concentrated and frequently contain other electrolytes under these conditions the activities of the pertinent species are much smaller than the concentrations, and consequently the use of the latter may lead to unreliable conclusions. Also, the actual active species present (see example below) may differ from those to which the ideal standard potentials apply. For these reasons formal potentials have been proposed to supplement standard potentials. The formal potential is the potential observed experimentally in a solution containing one mole each of the oxidised and reduced substances together with other specified substances at specified concentrations. It is found that formal potentials vary appreciably, for example, with the nature and concentration of the acid that is present. The formal potential incorporates in one value the effects resulting from variation of activity coefficients with ionic strength, acid-base dissociation, complexation, liquid-junction potentials, etc., and thus has a real practical value. Formal potentials do not have the theoretical significance of standard potentials, but they are observed values in actual potentiometric measurements. In dilute solutions they usually obey the Nernst equation fairly closely in the form ... [Pg.363]

For a dilute solution at high pressure, the variation of activity coefficient with pressure cannot be neglected. But when x2 is small, it is often a good approximation to assume, as above, that the activity coefficient is not significantly affected by composition. If we also assume that v2 the partial molar volume of the solute, is independent of both pressure and composition... [Pg.166]

Fig. 13. Plot of variations of activation energy ( /kJ mole"1) with water vapour pressure (PHjO/Torr) for dehydration of calcium sulphate. Data from Ball et al. [281,590, 591] who discuss the significance of these kinetic parameters. Dehydrations of CaS04 2 H2O, nucleation ( ), boundary (o) and diffusion (e) control Q-CaSC>4 5 H2O, diffusion control, below (X) and above (+) 415 K j3-CaS04 5 H20, diffusion control ( ). Fig. 13. Plot of variations of activation energy ( /kJ mole"1) with water vapour pressure (PHjO/Torr) for dehydration of calcium sulphate. Data from Ball et al. [281,590, 591] who discuss the significance of these kinetic parameters. Dehydrations of CaS04 2 H2O, nucleation ( ), boundary (o) and diffusion (e) control Q-CaSC>4 5 H2O, diffusion control, below (X) and above (+) 415 K j3-CaS04 5 H20, diffusion control ( ).
The variation of activation energy as a function of alloy composition is shown in Fig. 23. There is a fairly sharp rise in activation energy from about 0.4 kcal/mole at 50% Ag to 5.9 kcal/mole on pure Ag, but the increase observed with Pd-Au wires 127) was more abrupt. Pd-Ag alloy wires 148) showed a gradual increase from about 2 kcal/mole for pure Pd to 4 kcal/mole at 60% Ag, followed by a more rapid, smooth increase from 4.9 kcal/mole at 80% Ag to 11.5 kcal/mole on pure Ag. The results on films were also used to derive heats of adsorption at equilibrium coverage. Values increased from 1.29 kcal/mole on the 68% Ag alloy to 2.89 kcal/mole on pure Ag. [Pg.169]

The variation of activity (for ethylene oxidation) across the range of Pd-Rh alloy films (Fig. 27) followed in general the variation in apparent activation energy, although changes in activity were a consequence of... [Pg.174]

Plot these values of specific rates and interpret the variation of activation energy over the temperature range 500 to 1000 K. [Pg.211]

FIGURE 1.31 Variation of activation energy at different yttria concentrations. [Pg.38]

Though chemical purity is the topmost priority, yet the biological response of a pharmaceutical substance holds an equal importance. A wide variation of active ingredients ranging between 90% in one sample and 110% ( 10 per cent limit) in another sample could invariably be observed. Therefore, it has become absolutely essential to lay down definite standards so as to ensure that ... [Pg.5]

Jortner, J. Navon, G. J. Phys. Chem. 1981, 85, 3759]. On the other hand, if one considers the variation of activation energy with electronic energy gap, one finds a very large discrepancy between the quantum-mechanical and classical approaches for very exothermic reactions at room temperature (see Figure 1). [Pg.252]

Other variations of activated sludge such as deep shaft high-rate activated sludge and sequencing batch reactor (SBR) have been used for refinery wastewater treatment. A refined deep shaft process has been installed and in operation at the Chevron refinery in Burnaby, British Columbia, Canada, since 1996 [45]. In the course of a recent wastewater treatment upgrade, a BP refinery on the eastern Australian coast converted an existing lagoon to an SBR system [46]. [Pg.286]

Figure 7.16 Variation of activity for O2 evolution as a function of electrolysis time for continuous and intermittent electrolysis [65]. Figure 7.16 Variation of activity for O2 evolution as a function of electrolysis time for continuous and intermittent electrolysis [65].
This important piece of work had four main facets first, it showed that structure could be quantitatively related to biological activity secondly, it introduced the concept of activity being described by more than one parameter thirdly, the two-stage variation of activity wim the water-octanol partition coefficioit, denot by logP, was quantified using a quadratic equation and fourthly, it introduced the concept of the... [Pg.100]

The affinity of the polymer-bound catalyst for water and for organic solvent also depends upon the structure of the polymer backbone. Polystyrene is nonpolar and attracts good organic solvents, but without ionic, polyether, or other polar sites, it is completely inactive for catalysis of nucleophilic reactions. The polar sites are necessary to attract reactive anions. If the polymer is hydrophilic, as a dextran, its surface must be made less polar by functionalization with lipophilic groups to permit catalytic activity for most nucleophilic displacement reactions. The % RS and the chemical nature of the polymer backbone affect the hydrophilic/lipophilic balance. The polymer must be able to attract both the reactive anion and the organic substrate into its matrix to catalyze reactions between the two mutually insoluble species. Most polymer-supported phase transfer catalysts are used under conditions where both intrinsic reactivity and intraparticle diffusion affect the observed rates of reaction. The structural variables in the catalyst which control the hydrophilic/lipophilic balance affect both activity and diffusion, and it is often not possible to distinguish clearly between these rate limiting phenomena by variation of active site structure, polymer backbone structure, or % RS. [Pg.57]

In view of this complexity and the evident interrelation between reaction and self-poisoning, it is actually less surprising that the literature does not offer a clear picture of the particle size effects in the HC reactions. Hydro-genolysis of ethane by Pt and lr reveals a decrease in TON by a factor of 10-15, when the dispersion D is increased (antipathic relation) from %0.1 to 0.8 (231). An early paper on ethane hydrogenolysis by Ni reports a strong and a later paper reports a less pronounced variation of activity with D. However, in contrast to Pt and lr, this variation is always a sympathetic one (232, 233). The same holds true for Rh (234). [Pg.183]

The selectivity for citronellal increases up to a value of 81% (at 100% canv.) for a Sn/Rh ratio of 0.12. Above these values, the selectivity far citronellal decreases and the selectivity for geraniol and nerol increases up to 96% (at 100% conv.) for a Sn/Rh ratio of 0.92. Significant variations of activities are simultaneously observed suggesting selective metallic surface poisoning fallowed by enhanced catalytic activity due to a new catalytic material which contains a tin din-butyl fragment. [Pg.141]

Figure 26. Variation of activation energy with nitrogen percentage for samples obtained with different milling times... Figure 26. Variation of activation energy with nitrogen percentage for samples obtained with different milling times...

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Variation of catalytic activity

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